EP1803820B1 - A process for the preparation of vitamin K2 - Google Patents
A process for the preparation of vitamin K2 Download PDFInfo
- Publication number
- EP1803820B1 EP1803820B1 EP05425932A EP05425932A EP1803820B1 EP 1803820 B1 EP1803820 B1 EP 1803820B1 EP 05425932 A EP05425932 A EP 05425932A EP 05425932 A EP05425932 A EP 05425932A EP 1803820 B1 EP1803820 B1 EP 1803820B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- vitamin
- bacillus subtilis
- dsm
- fermentation
- culture
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/48—Hydrolases (3) acting on peptide bonds (3.4)
- C12N9/50—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
- C12N9/52—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from bacteria or Archaea
- C12N9/54—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from bacteria or Archaea bacteria being Bacillus
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/66—Preparation of oxygen-containing organic compounds containing the quinoid structure
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/20—Bacteria; Culture media therefor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
Definitions
- the present invention concerns the fermentative production of vitamin K2 (menaquinone - 7: MK - 7), using a Bacillus microorganism.
- the invention concerns a mutant of the microorganism Bacillus subtilis deposited under the Budapest Treaty, which is able to produce MK - 7 in high amounts, under specific culture conditions.
- Vitamin K is an essential cofactor for the formation of ⁇ -carboxyglutamic acid (Gla) residues in proteins (Olson, R.E., 1984 1 - Suttie, J.W., 1985 2 ).
- the Gla - containing proteins bind calcium ions and influence, for example, blood coagulation and tissue calcification (e.g., osteocalcin found in bone tissues) (Hauschka P.V. et al. 1978 3 - Price, P.A. et al., 1976 4 ).
- Vitamin K deficiency has been implicated in several clinical ailments such as intracranial hemorrhage in newborn infants (Ferland, G. et al., 1993 5 - Shearer, M.J., 1995 6 ) and possible bone fracture resulting from osteoporosis (Knapen, M.H. et al., 1989 7 ).
- Vitamin K occurs naturally in two forms, namely, K1 (phylloquinone) in green plants and K2 (menaquinones -MK) in animals and some bacteria (Collins, M.D. et al., 1981 8 - Conly, J.M. et al. 1992 9 - Ramotar, K. et al., 1984 10 - Taber, H. 1980 11 - Watanuki, M. et al. 1972 12 ), including intestinal bacteria.
- MK has a variable side chain length of 4 - 13 isoprene units. They are referred to as MK - ⁇ , where ⁇ denotes the number of isoprenoid residues.
- the MK are constituents of the bacterial plasma membrane and function as redox reagents in electron transport and oxidative phosphorylation systems (Taber, H. 1980 - Ramotar, K. et al. 1984).
- Lactic acid bacteria have been used as starter cultures to manufacture various foods and can be generally recognized as safe (GRAS), and a qualitative study has shown that some lactic acid bacteria produce MK. In many countries, the daily requirement for vitamin K is around 1 ⁇ g/kg of body weight.
- Yoshinori Tsukamoto et al. (2001) have recovered a analogous resistant mutant of B. subtilis "natto" having productivity of 1719 ⁇ g/100 g dry weight.
- K2 (MK - 7) is produced in amounts of 1.0 ⁇ g/g dry weight or below ( US 2004/043015 ; US 2005/0025759 ; US 2002/0146786 ; US 2001/0046697 ).
- Bacillus subtilis mutated strain having productivity ranging from 1,000 to 25,000 ppm of dry matter, with a production cycle (from pre-seed to fermentation) of 160 - 200 hours, more precisely 170 - 185 hours.
- the Bacillus subtilis mutant GN13/72 was obtained by treatments with NTG or, alternatively, U.V. and recovered on a micronised soy meal solid medium.
- the strain was deposited under the terms of the Budapest Treaty at the Deutsche Sammlung von Mikrorganismen und Zellkulturen (DSMZ) on December 5, 2005 under the accession number DSM 17766.
- the MK - 7 high-content biomass is prepared according to known fermentation techniques by means of culture media containing carbon sources (such as glucose, saccharose, glycerol, starch hydrolysate and the like); nitrogen sources (such as yeast extract or autolysate, peptones of various origin, soy meal and the like); various salts (such as potassium phosphate, sodium chloride, magnesium sulfate, manganese sulfate, zinc sulfate, and the like).
- carbon sources such as glucose, saccharose, glycerol, starch hydrolysate and the like
- nitrogen sources such as yeast extract or autolysate, peptones of various origin, soy meal and the like
- various salts such as potassium phosphate, sodium chloride, magnesium sulfate, manganese sulfate, zinc sulfate, and the like.
- the biomass is collected by centrifugation or microfiltration, washed twice with purified water and resuspended in purified water.
- the resulting creams are dried by freeze-drying or spray-drying, then packaged under vacuum.
- Bacillus subtilis GN13/27 - DSM 17766 is aerobically grown in a 30 l (geometrical) fermenter containing 20 l of "F10" fermentation medium having the following composition:
- the fermenter is inoculated with 8% (1600 ml) of 16h ( ⁇ 2 h) seed, whose "S3" medium has the following composition:
- the seed was in turn inoculated with 5 ml of B. subtilis suspension from a slant washed with 10 ml of purified water.
- the biomass obtained under said conditions was 8 ( ⁇ 1) g/l dry weight with MK - 7 content of 1100 ( ⁇ 100) ppm.
- Bacillus subtilis GN13/72 - DSM 17766 is cultured as in Example 1, the "F12" fermentation medium having the following composition:
- Bacillus subtilis GN13/72 - DSM 17766 is cultured as in Example 1, the "F13" fermentation medium having the following composition:
- Bacillus subtilis GN13/72 - DSM 17766 is cultured as in Example 3, the carbon source consisting of maltodextrin instead dextrin. Duration of the fermentation 140 h ( ⁇ 3 h). 8.0 ( ⁇ 1.0) g/l dry weight are obtained with MK - 7 content of 8500 ( ⁇ 150) ppm.
- Bacillus subtilis GN13/72 - DSM 17766 is cultured as in Example 4, the antifoam agent being soybean oil. Duration of the fermentation 144 h ( ⁇ 4 h). 11 ( ⁇ 1) g/l dry weight are obtained with MK - 7 content of 11700 ( ⁇ 300) ppm.
- Bacillus subtilis GN13/72 - DSM 17766 is cultured in a 300 l fermenter, with 225 l useful volume, medium "F13", pH automatically kept at 7.2 ( ⁇ 0.1) with NaOH; stirring 100 rpm; air 0.5 vvm; pressure 0.3 bar; antifoam soybean oil automatically controlled.
- Inoculum was 4% obtained in a seed of 30 l total with 20 l useful volume and "S3" medium (see Example 1).
- the biomass was divided into 2 parts: a part was freeze-dried to obtain a powder having 17000 ( ⁇ 350) ppm; the other part was spray-dried to obtain 20000 ( ⁇ 500) ppm.
- Example 7 The procedure of Example 7.is followed, in which the fermentation useful volume was 2 m 3 .
- the spray-dried final product was packaged in 250 g sachets under vacuum.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Medicinal Chemistry (AREA)
- Biomedical Technology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Virology (AREA)
- General Chemical & Material Sciences (AREA)
- Molecular Biology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Steroid Compounds (AREA)
Priority Applications (15)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE602005015133T DE602005015133D1 (de) | 2005-12-29 | 2005-12-29 | Verfahren zur Herstellung von Vitamin K2 |
| SI200530735T SI1803820T1 (sl) | 2005-12-29 | 2005-12-29 | Postopek za pripravo vitamina k2 |
| PT05425932T PT1803820E (pt) | 2005-12-29 | 2005-12-29 | Processo para a preparação de vitamina k2 |
| ES05425932T ES2326379T3 (es) | 2005-12-29 | 2005-12-29 | Procedimiento para la preparacion de vitamina k2. |
| EP05425932A EP1803820B1 (en) | 2005-12-29 | 2005-12-29 | A process for the preparation of vitamin K2 |
| PL05425932T PL1803820T3 (pl) | 2005-12-29 | 2005-12-29 | Sposób wytwarzania witaminy K2 |
| RSP-2009/0359A RS51172B (sr) | 2005-12-29 | 2005-12-29 | Proces za pripremanje vitamina k2 |
| AT05425932T ATE434666T1 (de) | 2005-12-29 | 2005-12-29 | Verfahren zur herstellung von vitamin k2 |
| DK05425932T DK1803820T3 (da) | 2005-12-29 | 2005-12-29 | Fremgangsmåde til fremstilling af vitamin K2 |
| US11/635,768 US7718407B2 (en) | 2005-12-29 | 2006-12-08 | Process for the preparation of vitamin K2 |
| KR1020060135200A KR101439473B1 (ko) | 2005-12-29 | 2006-12-27 | 비타민 k2의 제조 방법 |
| CA2572373A CA2572373C (en) | 2005-12-29 | 2006-12-28 | A process for the preparation of vitamin k2 |
| JP2006354565A JP5043425B2 (ja) | 2005-12-29 | 2006-12-28 | ビタミンk2の製造方法 |
| CY20091100829T CY1109266T1 (el) | 2005-12-29 | 2009-08-05 | Μεθοδος για την παρασκευη βιταμινης κ2 |
| HR20090507T HRP20090507T1 (hr) | 2005-12-29 | 2009-09-24 | Postupak priprave vitamina k2 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP05425932A EP1803820B1 (en) | 2005-12-29 | 2005-12-29 | A process for the preparation of vitamin K2 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1803820A1 EP1803820A1 (en) | 2007-07-04 |
| EP1803820B1 true EP1803820B1 (en) | 2009-06-24 |
Family
ID=36588821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP05425932A Expired - Lifetime EP1803820B1 (en) | 2005-12-29 | 2005-12-29 | A process for the preparation of vitamin K2 |
Country Status (15)
| Country | Link |
|---|---|
| US (1) | US7718407B2 (sr) |
| EP (1) | EP1803820B1 (sr) |
| JP (1) | JP5043425B2 (sr) |
| KR (1) | KR101439473B1 (sr) |
| AT (1) | ATE434666T1 (sr) |
| CA (1) | CA2572373C (sr) |
| CY (1) | CY1109266T1 (sr) |
| DE (1) | DE602005015133D1 (sr) |
| DK (1) | DK1803820T3 (sr) |
| ES (1) | ES2326379T3 (sr) |
| HR (1) | HRP20090507T1 (sr) |
| PL (1) | PL1803820T3 (sr) |
| PT (1) | PT1803820E (sr) |
| RS (1) | RS51172B (sr) |
| SI (1) | SI1803820T1 (sr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102010001832A1 (de) | 2010-02-11 | 2011-08-11 | Wacker Chemie AG, 81737 | Verfahren zur fermentativen Herstellung von Menachinon-7 mit Escherichia coli |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB0817528D0 (en) * | 2008-09-24 | 2008-10-29 | Syntavit As | Process |
| IN2009MU00380A (sr) * | 2009-02-18 | 2010-04-02 | ||
| DK2437758T3 (da) * | 2009-06-03 | 2014-07-21 | Chr Hansen As | Bakterie thyA(-) mutanter med forøget vitamin K |
| KR101196338B1 (ko) * | 2010-06-16 | 2012-11-01 | 무주군약초영농조합법인 | 비타민 k2 생성능이 높은 바실러스 아미로리퀴파시엔스 균주 |
| JP2014150731A (ja) * | 2013-02-05 | 2014-08-25 | Fuji Oil Co Ltd | メナキノン−7含有食品および微生物によるメナキノン−7の製造法 |
| WO2014131084A1 (en) * | 2013-02-27 | 2014-09-04 | The University Of Sydney | Fermentation and in situ extraction of menaquinones during microbial culture |
| JP6411586B2 (ja) * | 2016-06-15 | 2018-10-24 | アサヒグループホールディングス株式会社 | 骨代謝改善剤 |
| KR101875502B1 (ko) * | 2016-08-03 | 2018-07-09 | 민병규 | pH-스탯 방식의 유가식 배양을 이용한 바실러스 서브틸리스 균주로부터 비타민 K2의 생산방법 |
| US20220064678A1 (en) * | 2018-12-11 | 2022-03-03 | The Penn State Research Foundation | Method for production of vitamin k using biofilm reactors |
| CN110499345B (zh) * | 2019-09-02 | 2021-05-28 | 福建康鸿生物科技有限公司 | 一种维生素k2(MK-7型)的发酵方法 |
| KR102354881B1 (ko) * | 2019-10-30 | 2022-02-07 | 주식회사 지에프퍼멘텍 | 한국 전통 청국장에서 분리된 초고순도 트랜스형 메나퀴논-7 고생산능을 가지는 신규한 바실러스 서브틸리스 균주 및 이의 용도 |
| US11912654B2 (en) | 2021-09-03 | 2024-02-27 | Synergia Life Sciences Pvt. Ltd. | Process for stereospecific synthesis of vitamin K2 and its novel intermediates |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4843877B1 (sr) * | 1970-03-03 | 1973-12-21 | ||
| ES2007758A6 (es) * | 1987-12-07 | 1989-07-01 | Espanola Petrol | Un procedimiento para la obtencion de alfa-amilasas termoestables, por cultivo de microorganismos superproductores a altas temperaturas. |
| US5024937A (en) * | 1989-04-06 | 1991-06-18 | Dow Corning Corporation | Method for processing aqueous fermentation broths |
| JPH069474B2 (ja) * | 1990-03-20 | 1994-02-09 | 有限会社ビセイケン | アルコール耐性付与醗酵物の製造方法及びアルコール耐性付与醗酵食品 |
| US5525695A (en) * | 1991-10-15 | 1996-06-11 | The Dow Chemical Company | Elastic linear interpolymers |
| JP3272657B2 (ja) | 1998-01-19 | 2002-04-08 | シャープ株式会社 | スイッチング電源装置 |
| JP4068103B2 (ja) * | 1998-05-17 | 2008-03-26 | 洋行 須見 | 雲南sl−001菌の培養によるビタミンkの生産方法 |
| US6677141B2 (en) * | 1998-05-17 | 2004-01-13 | Honda Trading Corporation | Edible compositions of Bacillus subtilis natto cells containing water-soluble vitamin K |
| JP4104741B2 (ja) * | 1998-09-08 | 2008-06-18 | 旭松食品株式会社 | ビタミンk高生産性菌株及びそれを用いたビタミンkの生産方法 |
| JP4264159B2 (ja) * | 1999-04-07 | 2009-05-13 | 株式会社ミツカングループ本社 | ビタミンk2高生産性納豆菌、その育種方法及び納豆 |
| JP2001346546A (ja) * | 2000-06-08 | 2001-12-18 | Kikkoman Corp | ビタミンk濃縮物の製造方法 |
| JP2002034554A (ja) * | 2000-07-28 | 2002-02-05 | Mitsukan Group Honsha:Kk | ビタミンk2高生産納豆菌、その育種方法及び納豆 |
| JP2005237300A (ja) * | 2004-02-26 | 2005-09-08 | Aichi Prefecture | 食品素材及びその製造方法 |
-
2005
- 2005-12-29 RS RSP-2009/0359A patent/RS51172B/sr unknown
- 2005-12-29 PL PL05425932T patent/PL1803820T3/pl unknown
- 2005-12-29 AT AT05425932T patent/ATE434666T1/de active
- 2005-12-29 SI SI200530735T patent/SI1803820T1/sl unknown
- 2005-12-29 DE DE602005015133T patent/DE602005015133D1/de not_active Expired - Lifetime
- 2005-12-29 PT PT05425932T patent/PT1803820E/pt unknown
- 2005-12-29 DK DK05425932T patent/DK1803820T3/da active
- 2005-12-29 EP EP05425932A patent/EP1803820B1/en not_active Expired - Lifetime
- 2005-12-29 ES ES05425932T patent/ES2326379T3/es not_active Expired - Lifetime
-
2006
- 2006-12-08 US US11/635,768 patent/US7718407B2/en active Active
- 2006-12-27 KR KR1020060135200A patent/KR101439473B1/ko not_active Expired - Fee Related
- 2006-12-28 JP JP2006354565A patent/JP5043425B2/ja not_active Expired - Fee Related
- 2006-12-28 CA CA2572373A patent/CA2572373C/en active Active
-
2009
- 2009-08-05 CY CY20091100829T patent/CY1109266T1/el unknown
- 2009-09-24 HR HR20090507T patent/HRP20090507T1/hr unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102010001832A1 (de) | 2010-02-11 | 2011-08-11 | Wacker Chemie AG, 81737 | Verfahren zur fermentativen Herstellung von Menachinon-7 mit Escherichia coli |
| EP2360262A1 (de) | 2010-02-11 | 2011-08-24 | Wacker Chemie AG | Verfahren zur fermentativen Herstellung von Menachinon-7 mit Escherichia coli |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2572373A1 (en) | 2007-06-29 |
| JP5043425B2 (ja) | 2012-10-10 |
| CA2572373C (en) | 2014-02-04 |
| US7718407B2 (en) | 2010-05-18 |
| ES2326379T3 (es) | 2009-10-08 |
| DK1803820T3 (da) | 2009-10-12 |
| HRP20090507T1 (hr) | 2009-10-31 |
| KR20070072383A (ko) | 2007-07-04 |
| PL1803820T3 (pl) | 2009-12-31 |
| PT1803820E (pt) | 2009-07-14 |
| CY1109266T1 (el) | 2014-07-02 |
| SI1803820T1 (sl) | 2009-10-31 |
| EP1803820A1 (en) | 2007-07-04 |
| DE602005015133D1 (de) | 2009-08-06 |
| JP2007181461A (ja) | 2007-07-19 |
| KR101439473B1 (ko) | 2014-09-11 |
| RS51172B (sr) | 2010-10-31 |
| US20070154998A1 (en) | 2007-07-05 |
| ATE434666T1 (de) | 2009-07-15 |
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